|Número de publicación||US3585147 A|
|Tipo de publicación||Concesión|
|Fecha de publicación||15 Jun 1971|
|Fecha de presentación||1 Oct 1969|
|Fecha de prioridad||1 Oct 1969|
|También publicado como||DE2022390A1|
|Número de publicación||US 3585147 A, US 3585147A, US-A-3585147, US3585147 A, US3585147A|
|Cesionario original||Int Dioxcide Inc|
|Exportar cita||BiBTeX, EndNote, RefMan|
|Citada por (93), Clasificaciones (10)|
|Enlaces externos: USPTO, Cesión de USPTO, Espacenet|
June 15, 1971 G. GORDON 3,585,147
STABILIZED CHLORINE DIOXIDE SOLUTIONS CONTAININO A CHLORIDE AND PROCESSES OF MAKING AND USING SAME Filed Oct. 1, 1969 j 90 RELEASE OF c10 BY 5 N ADDITION OF SMALL 80 moums F mm AND ACID ems -00 ADDED/LITER NoCl LAJ H62 5g TIME vs. 0102 paooucnon 5 FOR ACID RELEASE OF d smmuzsn CHLORINE 5 No me: moxms i: g. F O 2 E 5 $2 1: l i l l I TIME (MIN) g 90- Q 3 so 5 5 Q 6 so g c s 2 so 5 a 31 $2 J pH INVENTOR H0 3 GILBERT eoanow FRACTION 0F STABILIZED CHLORINE DIOXIDE convemeo T0 CIOZ upon ACIDIFICATION By 5 QM mysnw VM" ATTORNEY5 United States Patent US. Cl. 252-187 12 Claims This application is a continuation-in-part of my application Ser. No. 711,024 filed Mar. 6, 1968, and now abandoned.
BACKGROUND OF INVENTION Chlorine dioxide is well known as a strong oxidizing agent which has many commercial and industrial applications. It is used for bleaching various organic materials such as pulp, textiles or flour; for treating water in food processing plants, cooling towers and other water supplies or effluents; as well as for other sterilizing, antiseptic and deodorizing purposes, including the treatment of various organic wastes, the combatting of pests, the preservation of various resins and glues, and many other cases where oxidizing power or microbiological control is helpful.
However, chlorine dioxide itself is a hazardous material to handle, unstable, and generally difficult to produce and to apply where needed. Even in aqueous solution, chlorine dioxide has chemical and physical characteristics such as an irritating, sharp odor which make many of its applications impractical. It is therefore most commonly used in the form of stabilized aqueous chlorine dioxide solutions or soluble chlorite salt solutions from which chlorine dioxide can be released by acidification. It is also sometimes used in latent form as a dry chlorite salt powder which is made by dehydrating such solutions and which likewise yields chlorine dioxide upon acidification.
Stabilization of aqueous solutions of chlorine dioxide by the addition of stabilizing agents which modify its characteristics sufficiently to make its use in industrial applications more attractive is known. Pat. No. 3,123,521, for example, discloses the stabilization of chlorine dioxide solutions with sodium carbonate peroxide.
It is also known that the chlorites of the alkali and alkaline earth metals, either in dry powder form or in aqueous solution decompose upon acidification to a certain extent to form chlorine dioxide. Pat. No. 2,071,091, for example, discloses such chlorite solutions.
However, when a stabilized chlorine dioxide or chlorite salt solution is acidified by the addition of an acid, such as sulfuric acid, the solution yields not only chlorine dioxide, but also sodium chlorate. Sodium chlorate is a relatively ineffective oxidizing agent as compared to chlorine dioxide. Thus, only a portion of the potential oxidizing power of such a solution is realized.
Further, it is often desirable in applications of chlorine dioxide to be able to control the release of chlorine dioxide from stabilized chlorine dioxide solutions. Although the rate of the release can be increased by increasing the acidity of the solution, increasing the concentration of 3,585,147 Patented June 15, 1971 stabilized chlorine dioxide, or by raising the temperature of the solution, the range of control which these factors provide is necessarily limited, and therefore it is desirable to provide for an even greater range of release of chlorine dioxide.
Still further, the previously known solutions of this type, when evaporated, have characteristically produced a dry metal chlorite residue which was highly explosive in contact with combustible material or on impact when in contact with metal. This hazard has also limited the utility of such solutions in some cases.
SUMMARY OF INVENTION Accordingly, the primary object of the present invention is to provide a chlorine dioxide release agent for use with solutions of chlorite salt or stabilized chlorine dioxide so as to essentially prevent or alleviate the problems of loss of oxidizing power, lack of control over chlorine dioxide release, and explosive hazard mentioned above.
Other and further objects of the present invention will be apparent to those skilled in the art from the following more detailed description.
The objects of the present invention are attained by including in aqueous solutions containing stabilized chlorine dioxide at least one chloride of a metal selected from the group consisting of the alkali metals and the alkaline earth metals.
It has been found that the aforesaid alkali metal and alkaline earth chlorides have a marked effect on the release of chlorine dioxide during the acidification of aqueous solutions of chlorite salt or stabilized chlorine dioxide and, thus, increase the oxidizing power of the acidified solution. Further, the addition of the chloride enhances both the rate and amount of production of chlorine dioxide and this affords a degree of control over the amounts of chlorine dioxide released in the solution.
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a graph showing the effect of added sodium chloride on the amount of chlorine dioxide released.
FIG. 2 is a graph showing the effect of added sodium chloride on the time needed for release of chlorine dioxide.
FIG. 3 is a graph showing the effect of pH on the amount of chlorine dioxide released.
DESCRIPTION OF PREFERRED EMBODIMENTS The improved aqueous solutions which will yield chlorine dioxide upon acidification may be, as previously has been indicated, solutions of stabilized chlorine dioxide such as chlorine dioxide solutions stabilized with sodium carbonate peroxide or sodium percarbonate, or solutions of a chlorite salt as such.
Stabilized chlorine dioxide solutions comprise aqueous solutions of reaction products of chlorine dioxide with alkaline peroxygen compounds. It appears that the alkaline peroxygen compounds stabilize the chlorine dioxide in solution by forming a more stable complex or compound, i.e., the corresponding chlorite, and thus give a more stable solution which has a longer shelf life as well as a solution containing a greater concentration of C10 than can be held in solution in the absence of a peroxygen compound.
Stabilized chlorine dioxide solutions of the kind disclosed and claimed in the aforementioned US. Pat. 3,123,- 521 are especially suitable for use as the chlorine dioxide yielding solutions which are improved in accordance with the present invention. However, aqueous solutions of chlorine dioxide which have been stabilized or converted to a chlorite with other alkaline peroxygen compounds are also suitable including those complexed with hydrogen peroxide and an alkali metal hydroxide or alkali salt such as an alkali metal bicarbonate, or an alkaline peroxygen compound such as sodium peroxide or sodium perborate. Generally speaking, when a sodium peroxygen compound is referred to as being useful herein, the corresponding compounds of potassium or lithium may be used as well.
Solutions of the stabilized or complexed chlorine dioxide may be prepared by dissolving the alkali metal peroxygen compound or compounds in water to form an aqueous solution containing about to percent, and preferably 8 to 13 percent, of the peroxygen compound, and then bubbling chlorine dioxide gas through the aqueous solution, preferably until at least about 40,000 p.p.m., and preferably between 50,000 and 75,000 p.p.m., of chlorine dioxide is absorbed therein. For good stability, the solution should be maintained at a pH value between about 7 and about 13 or higher, and preferably between 8 and 12.
In general, the chlorine dioxide gas which is to be used in the stabilized or complex solution should preferably be purified to remove all traces of free chlorine. There are several well-known techniques for accomplishing this separation. Chlorine gas is objectionable since, in aqueous solution, chlorine forms hypochlorous acid. Chlorine has a very sharp odor in concentrations as low as 3.5 parts per million. It is also extremely corrosive.
The alkali metal peroxygen stabilizing or complexing compounds are well known. The preferred ones include sodium carbonate peroxide or hydrogen peroxide with alkaline carbonates and bicarbonates, but alkali metal perborates may also be used if the toxicity imparted by the perborates is not objectionable.
Moreover, the present invention is similarly applicable to aqueous alkali metal chlorite solutions prepared by methods other than the stabilization of chlorine dioxide gas in water by a peroxygen compound, e.g., by direct solution of the appropriate dry chlorite salt in water or in dilute caustic.
The chlorides which are included in the aforesaid solutions are chlorides of alkali metal or alkaline earth metals. Sodium chloride and potassium chloride are preferred, but lithium chloride, calcium chloride, barium chloride, magnesium chloride and the like are also useful. It should be understood that for maximum effect such chlorides are best added to the stabilized chlorine dioxide solutions while the latter are at a pH of at least 5, or preferably 6 or higher, i.e., either before acidification or substantially concurrently therewith. Alternatively, the chloride can first be added to the water which is to be used in preparing the stabilized chlorine dioxide or chlorite solution.
As still another alternative, the chloride may be formed in situ by adding hydrochloric acid to a solution which contains an alkali metal hydroxide or carbonate or bicarbonate. Such chloride formation preferably is at least partially carried out while the pH of the stabilized chlorine dioxide or chlorite solution is at a pH of 5 or more, e.g., between 8 and 12, but additional chloride may be formed when the solution is acidified for the purpose of releasing the chlorine dioxide oxidant.
The chloride should be incorporated into the aqueous solution in an amount effective to increase the generation of chlorine dioxide. This will depend upon the solubility of the chloride as well as the concentration of stabilized chlorine dioxide or chlorite in solution. More particularly, the chloride can usefully be present in amounts from about 0.1 up to about gram moles per gram mole of dissolved chlorine dioxide. For example, the chloride can be present in amounts of from about 0.01 to 100 or even 300 grams, or preferably about 0.1 to grams, or most preferably 2 to 50 grams, per liter of stabilized chlorine dioxide solution. Higher or lower amounts may sometimes be necessary or desirable in increasing the release of chlorine dioxide or in repressing the formation of chlorate, as the optimum amount varies somewhat depending upon, for example, the chlorine dioxide concentration, acidity or temperature of the final 4 solution. The optimum is best det rmined by a few preliminary empirical tests.
Aqueous solutions of stabilized or complexed chlorine dioxide are stable as long as the solutions are substantially neutral or alkaline, as reflected by a pH of 7 or higher. However, if such solutions are acidified by the addition of a strong mineral acid, such as sulfuric acid, the solution will decompose to give mainly chlorine dioxide and sodium chlorate. In accordance with the present invention the amount of chlorine dioxide in terms of percentage of oxidizing power in final solution is greatly increased and the formation of chlorate is reduced.
Though the mechanism by which chlorine doxide is released when a chlorite salt is acidified is known to be complicated and many different reactions can take place in such a process, the mechanism can for the sake of convenience be adequately represented by the following series of hypothetical equations:
Surprisingly, when NaCl is admixed with the chlorite prior to or during the acidification step (1), step (3) which is responsibile for the unwanted chlorate formation is repressed.
The present invention is further illustrated by the following examples. In these examples as well as in all other parts of this specification and of the appended claims all parts and percentages of materials are given on a weight basis unless otherwise indicated.
EXAMPLE I A stabilized chlorine dioxide solution is prepared by dissolving powdered sodium carbonate peroxide in water to form a 10% solution. The stabilizing compound, sodium carbonate peroxide, is an addition compound of sodium carbonate and hydrogen peroxide, approximately corresponding to the formula 2Na CO -3H O This com pound as available commercially is a white powder containing 14% active oxygen and 29% hydrogen peroxide. Its solubility in water at 20 C. is 13.3%. In powdered form, the compound is relatively stable.
When the stabilized chlorine dioxide solution is intended to serve as a source of dry sodium chlorite upon evaporation, or when accidental evaporation to dryness in use is to be allowed for and the attendant explosive hazard is to be minimized, it is desirable to include between about 0.1 and 20, preferably between about 0.3 and 2, and most preferably between 0.5 and 1, moles sodium chloride or similar soluble hygroscopic chloride per mole of chlorine dioxide or chlorite present in the solution and to avoid exposing the dry residue to temperatures above about C. Solutions of sodium carbonate peroxide in water have characteristics similar to a solution prepared by separately dissolving hydrogen peroxide and sodium carbonate in water. The former solution, however, is more stable.
Chlorine dioxide gas which contains substantially no free chlorine is then bubbled through the solution of sodium carbonate peroxide. Approximately 568 mg. of gaseous chlorine dioxide is taken up per gram dry weight of sodium carbonate peroxide. A stabilized chlorine dioxide solution prepared in accordance with this method contains about 50,000 p.p.m. of chlorine dioxide at a pH value between 8 and 12.
This solution was then diluted 200 fold. In rapid succession sulfuric acid was added to obtain an acidity of 1.0 mole of hydrogen ions per liter of diluted solution and six grams of sodium chloride was then added per liter of diluted solution.
It was then found that 98% of the oxidizing power of this solution appeared as chlorine dioxide and only 2% as sodium chlorate.
On the other hand, for the same solution (200 times diluted), upon addition of the same amount of sulfuric (abs.) (e) (concentration) (path length) the C10 is thus determined. Samples were simultaneously added to sodium iodide solution in 0.1 M acid. The iodine formedis back titrated with standard thiosulfate solution. Thetiter of this solution gives the sum of the C10 and C10 (chlorite ion) concentrations. The spectrometric value for the C10 concentration is subtracted in order to obtain the C10 directly. A third sample of the Solution was added to excess sodium iodide, in the absence of air, in 6 M HCl. The iodine liberated was back titrated with standard thiosulfate solution. This titration gives the total oxidizing power, to wit, C10 C10; and C10 Thus the C10 concentration can be obtained by difference (titration 3-tritation 2).
EXAMPLES II-VI The results of Examples II through VI using varying amounts of sodium chloride are summarized in Table 1 and shown in FIG. 1. As in Example I, the initial solution containing 5 0,000 p.p.m. of stabilized chlorine dioxide was diluted 200 times, the indicated quantity of sodium chloride was added and the acidity for all examples was adjusted to 1.0 mole hydrogen ion per liter of solution. Similar results, in terms of percent oxidizing power, were found for 100, 200, 300, 400, and 500 times diluted solution, i.e., in solutions containing from less than 0.01% to 0.1% or even as much as 6 stabilized chlorine dioxide. The percent chlorine dioxide released from the stabilized chlorine dioxide solution does not appear to depend markedly on the dilution factor when protected by the addition of the soluble metal chloride.
TABLE 1 Release of C10; from stabilized solutions of chlorine dioxide by addition of acid and NaOl Grams N aCl Oxidizing power addletd per in final solution Additional data was collected to show the length of time needed for release of chlorine dioxide by the addition of acid alone as compared with the addition of acid plus one gram of sodium chloride per liter of solution of stabilized chlorine dioxide. A graph of typical results is shown in FIG. 2. The data for the graph of FIG. 2 were obtained with the 200 fold diluted solution of stabilized chlorine dioxide with enough sulfuric acid to give a pH of 2.0.
At the end of 5 minutes the acidified solution containing the added sodium chloride yielded more than twice as much C10 as the control solution yielded after the same interval, and yielded about the same amount of C10 as the control solution yielded after 40 minutes or more. At the end of the test period (about 50 minutes), about 50% more C10 was released when the solution was acidified in the presence of added chloride as compared with the control solution. In efiect, under these conditions more than 90% of the total potentially available C10 is released as such from the chloride containing solution by the end of 20 minutes whereas in the case of the control solution less than 80% of the total potentially available C10 is released by the end of 10 hours.
Additional data were also collected to show the effect of hydrogen ion concentration upon the percentage of stabilized chlorine dioxide released as chlorine dioxide. A graph of typical results is shown in FIG. 3. The data for the graph of FIG. 3 were obtained with a 300 fold dilution of the original stabilized chlorine dioxide prepared in Example I, at a temperature of about 25 C. At pH values above 3, the reaction becomes extremely slow, taking several days at such lower hydrogen ion concentrations and yielding primarily chlorate ions C10 with only a minor proportion of C10 At pH values below about 1.5 the reaction is rapid but as the pH is reduced below the optimum the ratio of released C10 to released chlorate tends to approach unity. The optimum pH depends somewhat on the temperature at which the solution is used, but quite generally a pH between 1 and 3, and particularly between 2 and 3, is about best. (CF/C10 ratios of greater than 10 could possibly also afiect the optimum by allowing the solutions to be more acid and still giving good yields.
EXAMPLE VII To illustrate the eiiect of the present invention on the explosive properties of the dry product, 100 ml. portions of solutions having the identical compositions as that of Example II (containing 2.5 g. NaCl per liter) and the Control (no NaCl) shown in Table 1, respectively, may be concentrated in porcelain dishes on a steam bath until solids begin to precipitate from solution and the concentrated solutions may then be evaporated to dryness in air.
The resulting solid residues or powders are then placed on a steel sheet and struck with a metal hammer. The residue from the Control solution detonates upon impact whereas the chloride-containing residue from the solution of Example 11 does not.
EXAMPLE VIII As shown below, the benefits which the present invention produces can be obtained not only when the alkali metal chloride is added as such to a previously formed stabilized chlorine dioxide or chlorite salt solution, but also when it is formed in situ, e.g., by the reaction of sodium carbonate and hydrochloric acid. The chloride salt can thus be included or formed in the peroxide-containing solution before chlorine dioxide is absorbed therein, or it can be included or formed therein after the chlorine dioxide has been dissolved and stabilized therein.
Accordingly, for instance, the invention may be practiced in any of the following ways.
(A) Include NaCl in absorbing solution before ClO absorption Dissolve 10 parts sodium carbonate peroxide (2Na CO 3H 0 and 10 parts sodium chloride in 100 parts demineralized water and bubble through the resulting solution a gas mixture containing about 5% by volume of chlorine-free chlorine dioxide in air at a temperature of about 25 C. until a solution containing 60,000 p.p.m. chlorine dioxide is formed. Upon acidification to a pH between 2 and 3, with or without substantial dilution, this solution is capable of releasing C10 at a high rate in a yield of or better, with only a very small yield of unwanted chlorate.
(B) Form NaCl in absorbing solution before C10 absorption Dissolve 120 grams sodium carbonate peroxide in 400 ml. distilled water and add more water to make 500 ml. of Solution I. This contains the equivalent of 16.8 grams active oxygen and 84 grams sodium bicarbonate.
Separately prepare Solution II by dissolving 133 grams sodium bicarbonate (1.58 mole) in about 375 grams water, slowly adding grams concentrated hydrochloric acid (36.5% HCl; 1.03 mole), and making up to 500 ml. with further addition of water. An aqueous solution containing about 1 mole NaCl and about 0.5 mole NaHCO is produced as the acid reacts with the bicarbonate.
When evolution of gas has stopped in Solution II, add Solution I to Solution II with agitation and make up to 1 liter With further addition of Water.
Bubble through resulting mixed solution in a glass column a gas mixture of chlorine-free C10 and air containing about 5% by volume C10 until the solution becomes saturated with ClO as indicated by C10 gas being present in the efiluent gases at the top of the column. The resulting solution will contain about 63,000 ppm. C10 in stabilized and free form. A small excess of free C10 is then stripped from the solution by aeration or aging until the C10 content becomes constant. The solution then is free of chlorate ions and hydrogen peroxide, but contains both stabilized chlorine dioxide (chlorite) and chloride ions.
This solution when acidified to a pH below 5, preferably between 2 and 3, with or without substantial dilution, again is capable of rapidly releasing more than 95% of its potential C10 content, with only a small yield of unwanted chlorate.
(C) Form NaCl in absorbing solution after C10 absorption Prepare 500 ml. of Solution 1 as in Procedure B above.
Separately prepare Solution III by dissolving 133 grams sodium bicarbonate in 375 grams water and making up to 500 ml. by further addition of water.
Add Solution I to Solution III with agitation and make up to 1 liter with further addition of water.
Bubble ClO -air mixture through the resulting mixed solution as in Procedure B until the solution becomes saturated with C10 (Solution IV).
Then slowly add 100 grams concentrated hydrochloric acid (36.5% HCl) to Solution IV with rapid stirring, thereby forming NaCl in the solution with evolution of carbon dioxide while leaving an excess of bicarbonate present. The evolution of carbon dioxide speeds the aging of the stabilized chlorine dioxide solution by helping to strip out excess free C10 but in all other respects the resulting solution has substantially the same properties and performance characteristics as the stabilized chlorine dioxide solution prepared by Procedure B.
While the invention has been illustrated above in terms of certain preferred embodiments, still other variations and modifications are of course possible within the scope and spirit of the present invention.
The invention is particularly defined and pointed out in the appended claims.
1. An aqueous solution containing stabilized chlorine dioxide dissolved therein in the form of an alkali metal chlorite at a pH between about 7 and 13 and adapted to release chlorine dioxide upon acidification to a pH of less than about 6, and a chloride of a metal selected from the group consisting of the alkali metals and the alkaline earth metals; said chloride present in an amount efiective to increase the release of said chlorine dioxide from said solution.
2. The composition of claim 1 wherein said solution contains the equivalent of from about 8 to about 13 percent sodium carbonate peroxide.
3. The composition of claim 1 wherein the pH is between about 8 and about 12, said stabilized chlorine dioxide is present in a concentration of more than 40,000 ppm. and said chloride is present in an amount providing 8 from about 0.1 to 20 moles chloride per mole of chlorine dioxide.
4. The composition of claim 1 wherein said chloride is sodium chloride present in an amount of from about 0.01 to 300 grams per liter of solution.
5. The composition of claim 1 wherein sodium chloride is present in a concentration between about 0.1 and 50 grams per liter.
6. A substantially dry, solid, detonation resistant alkali metal chlorite composition consisting essentially of between about 0.3 and 2 moles alkali metal chloride per mole of chlorite.
7. In the process of making an aqueous solution having a pH between about 8 and 12 and containing stabilized chlorine dioxide dissolved therein for release of gaseous chlorine dioxide upon acidification, the improvement Which comprises including a chloride of a metal selected from the group consisting of the alkali metals and the alkaline earth metals in said solution in an amount between 0.1 and 20 moles chloride per mole of chlorine dioxide and effective to increase the release of chlorine dioxide upon acidification.
8. A process for producing a stabilized chlorine dioxide solution which comprises passing ehlorine dioxide gas through an aqueous solution having a pH between about 7 and 13 and containing about 5 to 15 percent of a peroxygen compound and about 0.1 to 300* grams of an alkali metal chloride per liter.
9. A process according to claim 8 wherein said peroxygen compound is sodium carbonate peroxide and wherein sodium chloride is present in a concentration between about 0.1 and 50 grams per liter.
10. In the process of using an aqueous alkaline solu tion comprising stabilized chlorine dioxide dissolved therein for release of chlorine dioxide gas therefrom upon acidification, the improvement which comprises increasing the release of chlorine dioxide from the solution by adding a chloride of a metal selected from the group consisting of the alkali metals and the alkaline earth metals in an amount effective to increase the yield of liberated chlorine dioxide gas.
11. The process of claim 10 wherein said chlorine dioxide is present in said solution in a concentration greater than 40,000 ppm. ClO and in the form of sodium chlorite and wherein sodium chloride is included in said solution in an amount corresponding to about 0.1 to 20 moles per mole of dissolved C10 at a stage in the process when the solution is at a pH of not less than 6.
12. The process of claim 11 wherein said sodium chloride is added in an amount of from about 0.01 to 300 grams per liter of solution.
References Cited UNITED STATES PATENTS 2,833,624 5/1958 Sprauer 23l52 2,895,801 7/1959 Northgraves et al. 23152 2,936,219 5/1960 Rapson 23l52 3,123,521 3/1964 Wentworth et al. 252-187 3,278,447 10/1966 McNicholas 252187 RICHARD D. LOVERING, Primary Examiner IRWIN GLUCK, Assistant Examiner U.S. Cl. X.R. 8l08; 23-152
|Patente citante||Fecha de presentación||Fecha de publicación||Solicitante||Título|
|US3755068 *||26 Feb 1971||28 Ago 1973||Erco Envirotech Ltd||Regeneration of chlorine dioxide for pulp treatment|
|US3909194 *||16 May 1973||30 Sep 1975||Pulp Paper Res Inst||Bleaching of textiles with chlorine monoxide|
|US4084747 *||26 Mar 1976||18 Abr 1978||Howard Alliger||Germ killing composition and method|
|US4104190 *||21 Mar 1977||1 Ago 1978||Minnesota Mining And Manufacturing Company||Generation of chlorine dioxide for disinfection and sterilization|
|US4689215 *||29 Dic 1986||25 Ago 1987||Ratcliff Perry A||Method and composition for prevention and treatment of oral disease|
|US4690772 *||3 Jun 1985||1 Sep 1987||National Medical Care||Sterilant compositions|
|US4696811 *||29 Dic 1986||29 Sep 1987||Ratcliff Perry A||Method and composition for prevention and treatment of oral disease|
|US4786492 *||22 Jul 1987||22 Nov 1988||Ratcliff Perry A||Method and composition for prevention and treatment of oral disease|
|US4792442 *||22 Jul 1987||20 Dic 1988||Ratcliff Perry A||Method and composition for prevention and treatment of oral disease|
|US4793989 *||22 Jul 1987||27 Dic 1988||Ratcliff Perry A||Method and composition for prevention and treatment of oral disease|
|US4808389 *||22 Jul 1987||28 Feb 1989||Ratcliff Perry A||Method and composition for prevention and treatment of oral disease|
|US4818519 *||24 Ago 1987||4 Abr 1989||Ratcliff Perry A||Method and composition for prevention of plaque formation and plaque dependent diseases|
|US4837009 *||10 Mar 1987||6 Jun 1989||Ratcliff Perry A||Method and composition for prevention of plaque formation and plaque dependent diseases|
|US4851213 *||14 Sep 1988||25 Jul 1989||Ratcliff Perry A||Method and composition for prevention and treatment of oral disease due to S. Sanguis|
|US4855135 *||8 Dic 1988||8 Ago 1989||Ratcliff Perry A||Method for debriding|
|US4880638 *||23 Ago 1988||14 Nov 1989||Bioxy International, Ltd.||Biocidal composition and method for disinfecting articles|
|US4886657 *||2 Dic 1988||12 Dic 1989||Ratcliff Perry A||Method for preventing periodontitis|
|US4889714 *||2 Dic 1988||26 Dic 1989||Ratcliff Perry A||Method for retarding dental plaque by killing streptococcus sanguis|
|US4925656 *||2 Dic 1988||15 May 1990||Ratcliff Perry A||Method for retarding formation of dental plaque|
|US4929365 *||18 Sep 1989||29 May 1990||Phillips Petroleum Co.||Biofilm control|
|US4975285 *||2 Jun 1989||4 Dic 1990||Ratcliff Perry A||Method for cleaning dental prosthetic devices|
|US4978535 *||4 Oct 1988||18 Dic 1990||Ratcliff Perry A||Method for cleaning contact lenses|
|US5078908 *||2 Oct 1989||7 Ene 1992||Allergan, Inc.||Methods for generating chlorine dioxide and compositions for disinfecting|
|US5246662 *||30 Oct 1992||21 Sep 1993||Allergan, Inc.||Methods for generating chlorine dioxide and compositions for disinfecting|
|US5306440 *||30 Jun 1993||26 Abr 1994||Allergan, Inc.||Methods for generating chlorine dioxide and compositions for disinfecting|
|US5639295 *||3 Oct 1996||17 Jun 1997||Southwest Research Institute||Method of making a composition containing a stable chlorite source|
|US5648074 *||12 Dic 1994||15 Jul 1997||Allergan||Compositions and methods for disinfecting contact lenses and reducing proteinaceous deposit formation|
|US5695814 *||17 Jul 1996||9 Dic 1997||Southwest Research Institute||Method of making a powdered biocidal composition|
|US5696046 *||5 Sep 1996||9 Dic 1997||Green; Bruce Philip||Cold sterilant solution|
|US5705092 *||5 Jun 1995||6 Ene 1998||Southwest Research Institute||Multilayered biocidal film compositions|
|US5707739 *||5 Jun 1995||13 Ene 1998||Southwest Research Institute||Powdered biocidal compositions|
|US5736165 *||20 Jul 1994||7 Abr 1998||Allergan||In-the-eye use of chlorine dioxide-containing compositions|
|US5772986 *||8 Abr 1996||30 Jun 1998||Kross; Robert D.||Compositions and methods for reducing oral malodor|
|US5830511 *||23 Dic 1994||3 Nov 1998||Bioxy Inc.||Therapeutic, production and immunostimulatory uses of biocidal compositions|
|US5888528 *||19 May 1997||30 Mar 1999||Bernard Technologies, Inc.||Sustained release biocidal powders|
|US5914120 *||5 Sep 1997||22 Jun 1999||Southwest Research Institute||Amine-containing biocidal compositions containing a stabilized chlorite source|
|US5922776 *||4 Jun 1996||13 Jul 1999||Bernard Technologies, Inc.||Sustained release, transparent biocidal compositions|
|US5965264 *||29 Ago 1997||12 Oct 1999||Bernard Technologies, Inc.||Powders providing controlled sustained release of a gas|
|US5980826 *||3 Oct 1996||9 Nov 1999||Bernard Technologies Inc.||Methods of deodorizing and retarding contamination or mold growth using chlorine dioxide|
|US6004587 *||28 Oct 1998||21 Dic 1999||Bioxy Inc.||Therapeutic, production and immunostimulatory uses of biocidal compositions|
|US6007772 *||29 Jul 1997||28 Dic 1999||Green; Bruce Philip||Cold sterilant solution|
|US6024954 *||2 Ago 1996||15 Feb 2000||Allergan||Compositions and methods for disinfecting contact lenses and preserving contact lens care products|
|US6046243 *||19 May 1997||4 Abr 2000||Bernard Technologies, Inc.||Compositions for sustained release of a gas|
|US6096350 *||8 Sep 1995||1 Ago 2000||Alcide Corporation||Compositions and methods for prevention and treatment of diseases associated with honey bees|
|US6099855 *||21 Jun 1996||8 Ago 2000||Bioxy, Inc.||Therapeutic, production and immunostimulatory uses of biocidal compositions|
|US6277408||25 Ago 1999||21 Ago 2001||Southwest Research Institute||Silicate-containing powders providing controlled, sustained gas release|
|US6331514||7 May 1999||18 Dic 2001||Stephen R. Wurzburger||Sterilizing and disinfecting compound|
|US6488965||27 Nov 2000||3 Dic 2002||Hampar L. Karageozian||Synergistic antimicrobial preparations containing chlorite and hydrogen peroxide|
|US6592907||23 Jul 2001||15 Jul 2003||Hampar L. Karagoezian||Synergistic antimicrobial ophthalmic and dermatologic preparations containing chlorite and hydrogen peroxide|
|US6605304||21 Ago 1998||12 Ago 2003||Bernard Technologies, Inc.||Silicate-containing powders providing controlled, sustained gas release|
|US6814984||8 Feb 2002||9 Nov 2004||Clean Water International Llc||Frozen biocidal compositions and methods of use thereof|
|US7648716||26 Ene 2006||19 Ene 2010||Sk Pharmaceutical||Synergistic antimicrobial ophthalmic and dermatologic preparations containing chlorite and hydrogen peroxide|
|US7678388||16 Mar 2010||Mason John Y||Method of treating with chlorine dioxide|
|US7799227 *||14 Oct 2005||21 Sep 2010||Wp Engineering Limited||Method for hygienic operation of an ion exchanger|
|US8460701||2 Sep 2010||11 Jun 2013||S. K. Pharmaceuticals, Inc.||Synergistic antimicrobial preparations containing chlorite and hydrogen peroxide|
|US8765652||25 Jun 2012||1 Jul 2014||Gen-Probe Incorporated||Method of making a formulation for deactivating nucleic acids|
|US8784901||31 Dic 2013||22 Jul 2014||S.K. Pharmaceuticals, Inc.||Synergistic antimicrobial preparations containing chlorite and hydrogen peroxide|
|US8846357||20 Dic 2012||30 Sep 2014||E I Du Pont De Nemours And Company||Stabilized chlorine dioxide for contamination control in Zymomonas fermentation|
|US8992831||24 Sep 2010||31 Mar 2015||E. I. Du Pont De Nemours And Company||Stabilized chlorine dioxide to preserve carbohydrate feedstocks|
|US9072712||18 Jun 2014||7 Jul 2015||S.K. Pharmaceuticals, Inc.||Synergistic antimicrobial preparations containing chlorite and hydrogen peroxide|
|US9371556||4 Mar 2005||21 Jun 2016||Gen-Probe Incorporated||Solutions, methods and kits for deactivating nucleic acids|
|US20040037891 *||7 Jul 2003||26 Feb 2004||Karagoezian Hampar L.||Synergistic antimicrobial ophthalmic and dermatologic preparations containing chlorite and hydrogen peroxide|
|US20040104127 *||22 May 2003||3 Jun 2004||Rojas Juan Luis Araya||Process and composition for obtaining an aqueous chlorine dioxide ready for its use, stabilized in a carbonate buffer, being a powerful disinfecting agent with ecological, non residual non toxic and non phytotoxic cataloging in the concentrations of usage|
|US20050013763 *||11 May 2004||20 Ene 2005||Johnsondiversey, Inc.||System for producing and dispensing chlorine dioxide|
|US20050170016 *||18 Oct 2004||4 Ago 2005||Rose David C.||Frozen biocidal compositions and methods of use thereof|
|US20060068029 *||16 May 2005||30 Mar 2006||Mason John Y||Method of treating with chlorine dioxide|
|US20060127497 *||26 Ene 2006||15 Jun 2006||Karagoezian Hampar L|
|US20070104798 *||4 Dic 2006||10 May 2007||S.K. Pharmaceuticals, Inc.||Synergistic antimicrobial preparations containing chlorite and hydrogen peroxide|
|US20070264226 *||8 May 2007||15 Nov 2007||Karagoezian Hampar L||Synergistically enhanced disinfecting solutions|
|US20080031805 *||22 Abr 2005||7 Feb 2008||Wp Engineering Limited||Method For The Production Of Chlorine Dioxide|
|US20080110834 *||14 Oct 2005||15 May 2008||Wp Engineering Limited||Method for Hygienic Operation of an Ion Exchanger and Ion Exchanger System|
|US20090087897 *||1 Oct 2007||2 Abr 2009||Eric Guy Sumner||Prevention of bacterial growth in fermentation process|
|US20090324746 *||22 Jul 2009||31 Dic 2009||Bober Andrew M||System for producing and dispensing chlorine dioxide|
|US20100291649 *||18 May 2009||18 Nov 2010||E. I. Du Pont De Nemours And Company||Control of contaminant yeast in fermentation processes|
|US20110008420 *||13 Ene 2011||Karagoezian Hampar L||Synergistic antimicrobial preparations containing chlorite and hydrogen peroxide|
|US20110014276 *||2 Sep 2010||20 Ene 2011||Karagoezian Hampar L||Synergistic antimicrobial preparations containing chlorite and hydrogen peroxide|
|US20110024800 *||7 Oct 2010||3 Feb 2011||Hughes William A||Shared Resources in a Chip Multiprocessor|
|USRE31779 *||17 Abr 1980||25 Dic 1984||Alcide Corporation||Germ-killing composition and method|
|DE2728170A1 *||23 Jun 1977||4 Ene 1979||Lehmann Wilfried||Aq. chlorine di:oxide solns. - made by mixing solns. of sodium chlorite, sodium hypochlorite and sodium carbonate|
|DE2730883A1 *||8 Jul 1977||11 Ene 1979||Lehmann Wilfried||Chlorine-free aq. chlorine di:oxide soln. prepn. - by adding chlorite to water, acidifying, adding metal hydroxide and then carbonate|
|EP2786747A1 *||9 Ene 2012||8 Oct 2014||Xuewu Liu||Promoting hair growth solution containing chlorine dioxide preparation method and use method thereof|
|EP2786747A4 *||9 Ene 2012||15 Abr 2015||Xuewu Liu||Promoting hair growth solution containing chlorine dioxide preparation method and use method thereof|
|WO1990001876A1 *||17 Ago 1989||8 Mar 1990||Bioxy International, Ltd.||Biocidal compositions and method for disinfecting articles|
|WO1997008954A1 *||5 Sep 1996||13 Mar 1997||Alcide Corporation||Compositions and methods for prevention and treatment of diseases associated with honeybees|
|WO2000019981A1 *||6 Oct 1999||13 Abr 2000||Karagoezian Hampar L||Synergistic antimicrobial, dermatological and ophthalmic preparations containing chlorite and hydrogen peroxide|
|WO2005102920A1 *||22 Abr 2005||3 Nov 2005||Wp Engineering Limited||Method for the production of chlorine dioxide for disinfection purposes and preparation therefor|
|WO2006042702A1 *||14 Oct 2005||27 Abr 2006||Wp Engineering Limited||Method for the hygienic operation of an ion exchanger and ion exchange unit|
|WO2007050221A1 *||27 Sep 2006||3 May 2007||Selective Micro Technologies, Llc||Cleaning, sanitization and regeneration of chromatography media using chlorine dioxide|
|WO2011038317A1||27 Sep 2010||31 Mar 2011||E. I. Du Pont De Nemours And Company||Stabilized chlorine dioxide to preserve carbohydrate feedstocks|
|WO2012088180A1||20 Dic 2011||28 Jun 2012||E. I. Du Pont De Nemours And Company||Use of synergistic formulations containing stabilized chlorine dioxide and peroxide to reduce growth of contaminant microorganisms in ethanol fermentation|
|WO2012096766A1||20 Dic 2011||19 Jul 2012||E. I. Du Pont De Nemours And Company||Use of synergistic formulations containing stabilized chlorine dioxide and quaternary ammonium to reduce growth of contaminant microorganisms in ethanol fermentation|
|WO2014099509A1||11 Dic 2013||26 Jun 2014||E. I. Du Pont De Nemours And Company||Stabilized chlorine dioxide for contamination control in zymomonas fermentation|
|WO2016090213A1||4 Dic 2015||9 Jun 2016||E. I. Du Pont De Nemours And Company||Method of desulphitation of carbohydrates|
|Clasificación de EE.UU.||252/187.21, 8/108.1, 423/477|
|Clasificación internacional||C02F1/76, C01B11/00, C01B11/02|
|Clasificación cooperativa||C02F1/76, C01B11/024|
|Clasificación europea||C02F1/76, C01B11/02D2B|